CA1059326A - Steam condensing apparatus - Google Patents
Steam condensing apparatusInfo
- Publication number
- CA1059326A CA1059326A CA263,084A CA263084A CA1059326A CA 1059326 A CA1059326 A CA 1059326A CA 263084 A CA263084 A CA 263084A CA 1059326 A CA1059326 A CA 1059326A
- Authority
- CA
- Canada
- Prior art keywords
- steam
- tower
- outlet
- wet
- condenser
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
- F01K9/00—Plants characterised by condensers arranged or modified to co-operate with the engines
- F01K9/003—Plants characterised by condensers arranged or modified to co-operate with the engines condenser cooling circuits
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28B—STEAM OR VAPOUR CONDENSERS
- F28B1/00—Condensers in which the steam or vapour is separate from the cooling medium by walls, e.g. surface condenser
- F28B1/06—Condensers in which the steam or vapour is separate from the cooling medium by walls, e.g. surface condenser using air or other gas as the cooling medium
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28B—STEAM OR VAPOUR CONDENSERS
- F28B9/00—Auxiliary systems, arrangements, or devices
- F28B9/04—Auxiliary systems, arrangements, or devices for feeding, collecting, and storing cooling water or other cooling liquid
- F28B9/06—Auxiliary systems, arrangements, or devices for feeding, collecting, and storing cooling water or other cooling liquid with provision for re-cooling the cooling water or other cooling liquid
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28C—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA COME INTO DIRECT CONTACT WITHOUT CHEMICAL INTERACTION
- F28C1/00—Direct-contact trickle coolers, e.g. cooling towers
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
- Y02B30/70—Efficient control or regulation technologies, e.g. for control of refrigerant flow, motor or heating
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S165/00—Heat exchange
- Y10S165/162—Only direct-contact heat exchange between two separately supplied fluids
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S165/00—Heat exchange
- Y10S165/90—Cooling towers
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S261/00—Gas and liquid contact apparatus
- Y10S261/11—Cooling towers
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
STEAM CONDENSING APPARATUS
Abstract of the Disclosure There is disclosed apparatus for use in con-densing steam from the turbine exhaust of a power plant or the like, comprising a steam condenser having means for circulating cooling medium therethrough in order to condense a portion of the steam from the tur-bine exhaust, a wet cooling tower in which the cooling medium is cooled by means of ambient air, and a dry cooling tower in which the other portion of the steam is condensed by means of ambient air.
Abstract of the Disclosure There is disclosed apparatus for use in con-densing steam from the turbine exhaust of a power plant or the like, comprising a steam condenser having means for circulating cooling medium therethrough in order to condense a portion of the steam from the tur-bine exhaust, a wet cooling tower in which the cooling medium is cooled by means of ambient air, and a dry cooling tower in which the other portion of the steam is condensed by means of ambient air.
Description
~L~9S93Z6 This invention relates genera:Lly to apparatus '`
for use in condensing steam from the turbine exhaust of a power plant or the like wherein a portion of such steam is condensed within a steam condenser by means of cooling medium which in turn is cooled within a wet cooling tower section, and the other portion of the steam is condensed within a dry cooling tower section.
More particularly, it relates to improvements in appa-ratus of this type in which the wet tower may be removed from service during cool weather in order to conserve make-up water in areas where water i5 scarce~
As used herein, a "wet" cooling tower section includes fill over which the air is caused to pass, an inlet including means for causing a medium to be cooled to pass over the fill, and an outlet having a water basin to collect the medium beneath the fill, and a "dry" cooling tower section includes a tube hundle over ~ :
which the air is caused to pass, an inlet for introduc-ing a medium to be cooled into the bundle, and an outlet for withdrawing the medium from the bundle. In the case ; of both sections, air flow may be natural draft or mechanical draft which is forced or induced by fans.
: As used herein, a "steam condenser" includes a shell having an inlet to receive the steam, a hot well to collect the condensate, and means in~ermediate the ~,~, .
inlet and hot well for passing a cooling medium through the shell in heat exchange relation with the steam. Furthermore, -the condenser may be of the direct contact or mixiny type in which the medium is sprayed into -the shell and then withdrawn from the hot well, or it may be of the surface type in which the medium is circulated through tubes in the shell~ When two or more mediums are passed through the shell, and at least one is sprayed into the shell, the condenser is also known as a direct contact or mixing type. Still further, the condenser may include one or more shells, each having a hot well, and the cooling medium may be passed through each shell in parallel or series flow.
Owners of power plants prefer wet cooling tower sections inasmuch a~s they require less capital investme~t than dry cooliny tower sections. However, owners do not have th.is option if the source o~ make-up water for the wet section is limited. Hence, as set forth in the Balcke U.S.
Patent No. 3,635,042, it has been proposed to use combined wet-dry cooling tower sections, with the dry section being ; ;~
used at all times while the wet section is brought into use only during the warmer weather.
Fig. 1 of the Balcke patent shows apparatus of the particular type with which the present applica- i tion is concerned namely, wherein steam is condensed.
:
. . .
1 ~`' ,i, ' ~als93~
However, the wet and dry sections are built into a single tower, which requires that tower be of costly manufacture. Also, this arrangement of both sections ; in a single tower subjects tube bundles of the dry section to corrosion from the drift and water vapor from the wet section. Furthermore, if the circula-ting water flow is in series, as disclo~sed in certain of the embodiments of the Balcke apparatus, the dry section, which is vir~ually maintenance free, must be taken out of service during the frequent inspection and maintenance of the wet tower section. Still further, since both sections are built into the same tower, the design of each is controlled by the other insofar as air flow is concerned - i.e., either mechanical or natural draft.
In the above-described Balcke apparatus, con-densate from the dry cooling tower section is returned to the boiler throuqh a conduit connectirlg with the outlet conduit from the steam condenser. Thus, it would be necessary, in order to increase the plant cycle eficiency during cooler weather (when the wet tower is not in operation) by heatinq the condensate beore ; return to the boiler, preferably to saturation tempera-ture, to provide a heating tank, a storage hot well, and possibly separate condensate pumps.
An object of this invention is to provide apparatus of this type which permits the use of con-ventional cooling equipment.
, ., ..
:.
,.
.. . ..
~5~ 6 Another object is to provide such apparatus in which the dry tower section is not corroded by drift and water vapor from the wet tower section.
A further object is to provide such apparatus which does not require that the dry section be taken out of service during inspection and maintenance of the ~et section.
Still another object is to provide such appara-tus in which the type of air flow through each tower section may be best suited to that particular section.
Yet a further object is to provide such appa-ratus which is capable of accomplishing two or more of the foregoing objects.
Yet another ob~ect is to provide such appara-tus in which both condensate streams are handled with a single hot well and a sinsle set of condensate pumps.
A still further object is to provide appara-tus of the type described in the foregoing object in which condensate from the dry tower section is heated to saturation temperature, prior to return to the power cycle, lithout the need for a separate heat.ing tank.
These and other objects are accomplished, in accordance with the illustrated embodiment of the in-vention, by apparatus of this type in which each of the - 25 wet and dry cooling tower sections comprises an indi-vidual tower separate and distinct from the other to~er, thereby permitting each tower section to be of conven-tional, proven construction, preventing the dry tower ... .
..
~.' ' .
, ! .. ~ . .
35~
section from being corroded by drift and vapor from the separate and distinct wet tower, and enabling the dry tower section to be maintained in service while the wet tower section is being inspected and maintained.
Still further, the user of such apparatus has the op-tion of using the same or different types o~ air flow -i.e., mechanical or natural draft - in the two towers, depending on the economics.
In accordance with a further novel aspect of the present invention, the outlet from the tube bundle of the dry tower is connected with the steam condenser, so that condensate from the dry tower flows into the hot well of the condenser. More particularly, the connection is arranged to introduce the condensate into the steam zone of the condenser where it is dis-persed by suitable means such as sprays to cause it to intimately contact the steam before entering the condenser hot well. Thus, condensate from the dry tower is reheated to saturation temperature without the necessity of a separate heating tank, and both the wet and dry system~ ma~e use of a common hot well in each shell and condensate pumps, thereby resulting in a substantial cost saving. ;
Preferably, intimate con~act of the steam with the condensate is promoted by causing the conden-sate to cascade downwardly over the tubes within the condenser through which the cooling medium from the wet tower is adapted to be circulated. However, in order to avoid degradation of the cooling performance of the , 3~ ;
wet tower during warmer temperatures, and thus while cooling medium is circulating through the tubes, additional means are provided for introducing the condensate into the con- `
denser near the hot well during such warmer temperatures.
As will be appreciated,there is little need for reheating the condensate during these warmer temperat:ures since it is normally not subcooled to any degree.
In accordance with the above listed objects of the present invention, from a further broad aspect there is provided an apparatus for use in condensing steam from the turbine exhaust of a power plant or the like. The apparatus ~ ~
comprises means for receiving steam from the turbine exhaust ~ -and dividing it into first and second branches. ~ steam condenser i.s provided and has an inlet Eor receiviny s-team ~rom the ~irst branch. A hot well i9 provided to receive condensed steam and is also provided with an outlet. Means is provided for returning condensate from the outlet of the hot well. A wet cooling tower is provided including fill over which ambient air is caused to pass. An inlet is provided having means for spraying a cooling medium over the fill, and an outlet including a water basin is provided to collect the medium beneath the fill. Means connects the inlet and outlet ok the wet tower section with tubes within the steam condenser for circulating the medium through the tubes in heat exchange relation therewith. A dry cooling tower, separate from the wet tower, includes a tube bundle over which ambient air is ` caused to pass. An inlet is provided to -the bundle for receiving steam from the second branch, and an outlet is provided from the bundle. Means is further provided for returning condensate from the outlet of the bundle to the power cycle.
i ;. . ~ .
The embodiment of the apparatus illustrated in the single Figure of the drawings includes a steam duct or manifold 10 having an inlet adapted to receive steam from the turbine exhaust from a power plant or the like which is indicated diagrammatically at 11. The duct 10 has a first branch 12 leading to a surface type steam con-denser 13 in which a portion of the steam is condensed by .
means of a medium cooled within a wet type cooling tower 16, and a second branch 14 leading to a dry type cooling tower 15 in which the remaining portion of the steam iscondensed. As will be described to follow, condensate of the condensed steam within dry tower 15 is introducecl into the condenser 13, and returned to the power cycle wlth the condensate which is condensed in the condenser. The con-denser 13 as well as the duct 10 are dlsposed with:in thepower plant proper, while each of the dry and wet cooling towers 15 and 16, respectively, are supporting on ground :
level G outside of the plant. .
Condenser 13 comprises a shell 17 having an .-~
inlet in its right side for connection with branch -7a-." ''''"' '''"'''''''''''' '' ~' :'' "
-' ~l05~3~6 12 of housing 10, and a hot well 18 in its lower end for collecting steam which is condensed therein as well as that which is condensed within the dry tower and introduced into the shell. Condensate is returned to the power cycle by means of a pump 20 disposed within a conduit 19 connecting an outlet from the shell in the lower end of the hot well. The surface ~ -:, - .
condenser also includes tubes 21 disposed within the ;~
shell 17 which circulate cooling medium cooled in wet tower 16 in heat exchange relation with the steam entering the condenser shell through branch 12.
A~ previously described, during cold weather, `
when the wet tower is out o~ service and thus cool water or other medium is not being circulated through tubes 21, condensate from the dry tower 15 is intro-duced into the steam zone of the condenser shell, and, more particularly, above tubes 21 by me~ns of spray heads 23 mounted on a manifold 22 or perforations in the manifold. Thus, as previously mentioned, the con-densate is caused to cascade over the tubes and thusto be intimately contacted by the steam as it passes downwardly into the hot well 18, where it is collected with condensate of the steam condensed in the shell of the condenser 13. During warm weather, however, when ;
the wet tower is in service and thus a cooling medium is circulating through the tubes, condensate from dry tower 15 is instead introduced into the condenser shell near the hot well. In this way, the condensate is kept .. , .:.
'i out of contact with the tubes so as to avoid degxading ' . ,.
,: .'' ' ' ~05~
the heat exchange capacity thereof. In either event, the condensate is returned to the power cycle through the same hot well and with the same pu~p (or sets of hot wells and p~nps in the case of multiple shells) as the steam is condensed in the shell.
As shown, dry tower 15 is of the induced draft type comprising a housing 25 having at least one bundle of tubes 26 extending thereacross, and a an 27 mounted in its open upper end. The housing is mounted on legs 28 with its open lower end above ground level G so that ambient air is drawn upwardly over the bundle o tubes 26 as it is drawn upwardly ;~
through the fan 27.
The second branch 14 of duct 10 connects with an inlet to a header 29 on one end of the bundle, and another header 30 connects with the opposite end of the bundle so as to receive condensate of the steam condensed in the tubes. A conduit 31 connecting the lower end of an outlet from the header 30 is in turn connected with branches 31A and 31B leading, respect-ively, to the manifold 22 extending into the condenser shell, and to the hot well 18.
As shown, there i5 a valve 31A' in branch 31A
and a valve 31B' in branch 31B. Thus, during cold weather, valve 31A' may be closed and valve 31B' opened to cause condensate to be introduced directly into ~he hot well.
Then, during warm weather, valve 31A' may be opened and valve 31B' closed to cause condensate to be introduced into the steam zone of the condenser above tubes 21.
_g_ ~05~Z~
Wet cooling tower 16 is also of the induced draft type comprising a housing 32 having louvers 33 at its opposite sides and a fan 34 mounted on its open upper end. Fill 34a is mounted within l:he housing be-neath the fan 34 and opposite the louvers 33, so thatambient air is caused to pass therethrough as it is drawn through the louvers upwardly through the upper end of the housing.
The raw water to be cooled in the wet tower is introduced into a manifold 35 extending into the housing above the fill 34a and sprayed onto the fill by means of heads 36 mounted on the manifold. Thus, the water is caused to flow over the fill and into a water basin 37 in the lower end of the housing. The water is introduc~d into the manifold by means of a conduit 38 connecting with the upper ends of tubes 21, and is ~ithdrawn from the water basin by means of a con-duit 39 connecting with the lower ends of ~he tubes. A
pump 40 is disposed within conduit 3g so that, as indi-cated by the arrows in the drawing, the water is cir-culated through the wet tower and into and through the tubes in surface condenser 13, for purposes previously described.
Although each of the wet and dry towers is shown to be of the induced draft type, it will be understood that either or both may instead be of a natural draft type. It will also be understood that although steam condenser 13 is shown to comprise a single shell, it may comprise two or more shells, in .
' ~L0~93Z6 , "
which case, of course, there would be a corresponding number of sections of tubes 21. Also, of course, the tubes may be connected either in parallel or series.
As previously described, this invention con-S templates that dry tower 15 will be in service at all times, while the wet tower 16 may be removed from service during cooler weather, as by stopping of pump -~
40 so as to interrupt circulation of cooling medium ~
through the condenser 13. On the other hand, during -hot weather, the wet tower will be in service. During cold weather, the capacity of the dry tower may be reduced, as by conventional means, such as adjustment of the fan 27, louvered air openings into the housing, sectionalized tube bundles permitting individual lS bundles to be removed from service, or the like.
From the foregoing it will be seen that this invention is one well adapted to attain all of the ends `
and objects hereinabove set forth, together with other advantages which are obvious and which are inherent to the apparatus.
It will be understood that certain features and suhcombination~ are of utility and may be employed without reference to other features and subcombinations.
This is contemplated by and is within the scope of the ... .
claims.
As many possible embodiments may be made of the invention without departing from the scope thereof, it is to be understood that all matter herein set forth or shown in the accompanying drawings is to be inter-; preted as illustrative and not in a limiting sense.
,',. ' ., :
:
~, :
for use in condensing steam from the turbine exhaust of a power plant or the like wherein a portion of such steam is condensed within a steam condenser by means of cooling medium which in turn is cooled within a wet cooling tower section, and the other portion of the steam is condensed within a dry cooling tower section.
More particularly, it relates to improvements in appa-ratus of this type in which the wet tower may be removed from service during cool weather in order to conserve make-up water in areas where water i5 scarce~
As used herein, a "wet" cooling tower section includes fill over which the air is caused to pass, an inlet including means for causing a medium to be cooled to pass over the fill, and an outlet having a water basin to collect the medium beneath the fill, and a "dry" cooling tower section includes a tube hundle over ~ :
which the air is caused to pass, an inlet for introduc-ing a medium to be cooled into the bundle, and an outlet for withdrawing the medium from the bundle. In the case ; of both sections, air flow may be natural draft or mechanical draft which is forced or induced by fans.
: As used herein, a "steam condenser" includes a shell having an inlet to receive the steam, a hot well to collect the condensate, and means in~ermediate the ~,~, .
inlet and hot well for passing a cooling medium through the shell in heat exchange relation with the steam. Furthermore, -the condenser may be of the direct contact or mixiny type in which the medium is sprayed into -the shell and then withdrawn from the hot well, or it may be of the surface type in which the medium is circulated through tubes in the shell~ When two or more mediums are passed through the shell, and at least one is sprayed into the shell, the condenser is also known as a direct contact or mixing type. Still further, the condenser may include one or more shells, each having a hot well, and the cooling medium may be passed through each shell in parallel or series flow.
Owners of power plants prefer wet cooling tower sections inasmuch a~s they require less capital investme~t than dry cooliny tower sections. However, owners do not have th.is option if the source o~ make-up water for the wet section is limited. Hence, as set forth in the Balcke U.S.
Patent No. 3,635,042, it has been proposed to use combined wet-dry cooling tower sections, with the dry section being ; ;~
used at all times while the wet section is brought into use only during the warmer weather.
Fig. 1 of the Balcke patent shows apparatus of the particular type with which the present applica- i tion is concerned namely, wherein steam is condensed.
:
. . .
1 ~`' ,i, ' ~als93~
However, the wet and dry sections are built into a single tower, which requires that tower be of costly manufacture. Also, this arrangement of both sections ; in a single tower subjects tube bundles of the dry section to corrosion from the drift and water vapor from the wet section. Furthermore, if the circula-ting water flow is in series, as disclo~sed in certain of the embodiments of the Balcke apparatus, the dry section, which is vir~ually maintenance free, must be taken out of service during the frequent inspection and maintenance of the wet tower section. Still further, since both sections are built into the same tower, the design of each is controlled by the other insofar as air flow is concerned - i.e., either mechanical or natural draft.
In the above-described Balcke apparatus, con-densate from the dry cooling tower section is returned to the boiler throuqh a conduit connectirlg with the outlet conduit from the steam condenser. Thus, it would be necessary, in order to increase the plant cycle eficiency during cooler weather (when the wet tower is not in operation) by heatinq the condensate beore ; return to the boiler, preferably to saturation tempera-ture, to provide a heating tank, a storage hot well, and possibly separate condensate pumps.
An object of this invention is to provide apparatus of this type which permits the use of con-ventional cooling equipment.
, ., ..
:.
,.
.. . ..
~5~ 6 Another object is to provide such apparatus in which the dry tower section is not corroded by drift and water vapor from the wet tower section.
A further object is to provide such apparatus which does not require that the dry section be taken out of service during inspection and maintenance of the ~et section.
Still another object is to provide such appara-tus in which the type of air flow through each tower section may be best suited to that particular section.
Yet a further object is to provide such appa-ratus which is capable of accomplishing two or more of the foregoing objects.
Yet another ob~ect is to provide such appara-tus in which both condensate streams are handled with a single hot well and a sinsle set of condensate pumps.
A still further object is to provide appara-tus of the type described in the foregoing object in which condensate from the dry tower section is heated to saturation temperature, prior to return to the power cycle, lithout the need for a separate heat.ing tank.
These and other objects are accomplished, in accordance with the illustrated embodiment of the in-vention, by apparatus of this type in which each of the - 25 wet and dry cooling tower sections comprises an indi-vidual tower separate and distinct from the other to~er, thereby permitting each tower section to be of conven-tional, proven construction, preventing the dry tower ... .
..
~.' ' .
, ! .. ~ . .
35~
section from being corroded by drift and vapor from the separate and distinct wet tower, and enabling the dry tower section to be maintained in service while the wet tower section is being inspected and maintained.
Still further, the user of such apparatus has the op-tion of using the same or different types o~ air flow -i.e., mechanical or natural draft - in the two towers, depending on the economics.
In accordance with a further novel aspect of the present invention, the outlet from the tube bundle of the dry tower is connected with the steam condenser, so that condensate from the dry tower flows into the hot well of the condenser. More particularly, the connection is arranged to introduce the condensate into the steam zone of the condenser where it is dis-persed by suitable means such as sprays to cause it to intimately contact the steam before entering the condenser hot well. Thus, condensate from the dry tower is reheated to saturation temperature without the necessity of a separate heating tank, and both the wet and dry system~ ma~e use of a common hot well in each shell and condensate pumps, thereby resulting in a substantial cost saving. ;
Preferably, intimate con~act of the steam with the condensate is promoted by causing the conden-sate to cascade downwardly over the tubes within the condenser through which the cooling medium from the wet tower is adapted to be circulated. However, in order to avoid degradation of the cooling performance of the , 3~ ;
wet tower during warmer temperatures, and thus while cooling medium is circulating through the tubes, additional means are provided for introducing the condensate into the con- `
denser near the hot well during such warmer temperatures.
As will be appreciated,there is little need for reheating the condensate during these warmer temperat:ures since it is normally not subcooled to any degree.
In accordance with the above listed objects of the present invention, from a further broad aspect there is provided an apparatus for use in condensing steam from the turbine exhaust of a power plant or the like. The apparatus ~ ~
comprises means for receiving steam from the turbine exhaust ~ -and dividing it into first and second branches. ~ steam condenser i.s provided and has an inlet Eor receiviny s-team ~rom the ~irst branch. A hot well i9 provided to receive condensed steam and is also provided with an outlet. Means is provided for returning condensate from the outlet of the hot well. A wet cooling tower is provided including fill over which ambient air is caused to pass. An inlet is provided having means for spraying a cooling medium over the fill, and an outlet including a water basin is provided to collect the medium beneath the fill. Means connects the inlet and outlet ok the wet tower section with tubes within the steam condenser for circulating the medium through the tubes in heat exchange relation therewith. A dry cooling tower, separate from the wet tower, includes a tube bundle over which ambient air is ` caused to pass. An inlet is provided to -the bundle for receiving steam from the second branch, and an outlet is provided from the bundle. Means is further provided for returning condensate from the outlet of the bundle to the power cycle.
i ;. . ~ .
The embodiment of the apparatus illustrated in the single Figure of the drawings includes a steam duct or manifold 10 having an inlet adapted to receive steam from the turbine exhaust from a power plant or the like which is indicated diagrammatically at 11. The duct 10 has a first branch 12 leading to a surface type steam con-denser 13 in which a portion of the steam is condensed by .
means of a medium cooled within a wet type cooling tower 16, and a second branch 14 leading to a dry type cooling tower 15 in which the remaining portion of the steam iscondensed. As will be described to follow, condensate of the condensed steam within dry tower 15 is introducecl into the condenser 13, and returned to the power cycle wlth the condensate which is condensed in the condenser. The con-denser 13 as well as the duct 10 are dlsposed with:in thepower plant proper, while each of the dry and wet cooling towers 15 and 16, respectively, are supporting on ground :
level G outside of the plant. .
Condenser 13 comprises a shell 17 having an .-~
inlet in its right side for connection with branch -7a-." ''''"' '''"'''''''''''' '' ~' :'' "
-' ~l05~3~6 12 of housing 10, and a hot well 18 in its lower end for collecting steam which is condensed therein as well as that which is condensed within the dry tower and introduced into the shell. Condensate is returned to the power cycle by means of a pump 20 disposed within a conduit 19 connecting an outlet from the shell in the lower end of the hot well. The surface ~ -:, - .
condenser also includes tubes 21 disposed within the ;~
shell 17 which circulate cooling medium cooled in wet tower 16 in heat exchange relation with the steam entering the condenser shell through branch 12.
A~ previously described, during cold weather, `
when the wet tower is out o~ service and thus cool water or other medium is not being circulated through tubes 21, condensate from the dry tower 15 is intro-duced into the steam zone of the condenser shell, and, more particularly, above tubes 21 by me~ns of spray heads 23 mounted on a manifold 22 or perforations in the manifold. Thus, as previously mentioned, the con-densate is caused to cascade over the tubes and thusto be intimately contacted by the steam as it passes downwardly into the hot well 18, where it is collected with condensate of the steam condensed in the shell of the condenser 13. During warm weather, however, when ;
the wet tower is in service and thus a cooling medium is circulating through the tubes, condensate from dry tower 15 is instead introduced into the condenser shell near the hot well. In this way, the condensate is kept .. , .:.
'i out of contact with the tubes so as to avoid degxading ' . ,.
,: .'' ' ' ~05~
the heat exchange capacity thereof. In either event, the condensate is returned to the power cycle through the same hot well and with the same pu~p (or sets of hot wells and p~nps in the case of multiple shells) as the steam is condensed in the shell.
As shown, dry tower 15 is of the induced draft type comprising a housing 25 having at least one bundle of tubes 26 extending thereacross, and a an 27 mounted in its open upper end. The housing is mounted on legs 28 with its open lower end above ground level G so that ambient air is drawn upwardly over the bundle o tubes 26 as it is drawn upwardly ;~
through the fan 27.
The second branch 14 of duct 10 connects with an inlet to a header 29 on one end of the bundle, and another header 30 connects with the opposite end of the bundle so as to receive condensate of the steam condensed in the tubes. A conduit 31 connecting the lower end of an outlet from the header 30 is in turn connected with branches 31A and 31B leading, respect-ively, to the manifold 22 extending into the condenser shell, and to the hot well 18.
As shown, there i5 a valve 31A' in branch 31A
and a valve 31B' in branch 31B. Thus, during cold weather, valve 31A' may be closed and valve 31B' opened to cause condensate to be introduced directly into ~he hot well.
Then, during warm weather, valve 31A' may be opened and valve 31B' closed to cause condensate to be introduced into the steam zone of the condenser above tubes 21.
_g_ ~05~Z~
Wet cooling tower 16 is also of the induced draft type comprising a housing 32 having louvers 33 at its opposite sides and a fan 34 mounted on its open upper end. Fill 34a is mounted within l:he housing be-neath the fan 34 and opposite the louvers 33, so thatambient air is caused to pass therethrough as it is drawn through the louvers upwardly through the upper end of the housing.
The raw water to be cooled in the wet tower is introduced into a manifold 35 extending into the housing above the fill 34a and sprayed onto the fill by means of heads 36 mounted on the manifold. Thus, the water is caused to flow over the fill and into a water basin 37 in the lower end of the housing. The water is introduc~d into the manifold by means of a conduit 38 connecting with the upper ends of tubes 21, and is ~ithdrawn from the water basin by means of a con-duit 39 connecting with the lower ends of ~he tubes. A
pump 40 is disposed within conduit 3g so that, as indi-cated by the arrows in the drawing, the water is cir-culated through the wet tower and into and through the tubes in surface condenser 13, for purposes previously described.
Although each of the wet and dry towers is shown to be of the induced draft type, it will be understood that either or both may instead be of a natural draft type. It will also be understood that although steam condenser 13 is shown to comprise a single shell, it may comprise two or more shells, in .
' ~L0~93Z6 , "
which case, of course, there would be a corresponding number of sections of tubes 21. Also, of course, the tubes may be connected either in parallel or series.
As previously described, this invention con-S templates that dry tower 15 will be in service at all times, while the wet tower 16 may be removed from service during cooler weather, as by stopping of pump -~
40 so as to interrupt circulation of cooling medium ~
through the condenser 13. On the other hand, during -hot weather, the wet tower will be in service. During cold weather, the capacity of the dry tower may be reduced, as by conventional means, such as adjustment of the fan 27, louvered air openings into the housing, sectionalized tube bundles permitting individual lS bundles to be removed from service, or the like.
From the foregoing it will be seen that this invention is one well adapted to attain all of the ends `
and objects hereinabove set forth, together with other advantages which are obvious and which are inherent to the apparatus.
It will be understood that certain features and suhcombination~ are of utility and may be employed without reference to other features and subcombinations.
This is contemplated by and is within the scope of the ... .
claims.
As many possible embodiments may be made of the invention without departing from the scope thereof, it is to be understood that all matter herein set forth or shown in the accompanying drawings is to be inter-; preted as illustrative and not in a limiting sense.
,',. ' ., :
:
~, :
Claims
1. Apparatus for use in condensing steam from the turbine exhaust of a power plant or the like, comprising means for receiving steam from the turbine exhaust and dividing it into first and second branches, a steam condenser having an inlet for receiving steam from the first branch, a hot well to receive condensed steam, and an outlet from the hot well, means for returning condensate from the outlet to the power cycle, a wet cooling tower including fill over which ambient air is caused to pass, an inlet having means for spraying a cooling medium over the fill, and an outlet including a water basin to collect the medium beneath the fill, means connect-ing the inlet and outlet of the wet tower section with tubes within the steam condenser for circulating said medium through the tubes in heat exchange relation therewith, a dry cooling tower separate from the wet tower including a tube bundle over which ambient air is caused to pass, an inlet to the bundle for receiving steam from the second branch, and an outlet from the bundle, and means for returning condensate from the outlet of the bundle to the power cycle.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA313,873A CA1063362A (en) | 1976-05-28 | 1978-10-20 | Steam condensing apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US05/690,883 US4296802A (en) | 1975-06-16 | 1976-05-28 | Steam condensing apparatus |
Publications (1)
Publication Number | Publication Date |
---|---|
CA1059326A true CA1059326A (en) | 1979-07-31 |
Family
ID=24774369
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA263,084A Expired CA1059326A (en) | 1976-05-28 | 1976-10-08 | Steam condensing apparatus |
CA313,873A Expired CA1063362A (en) | 1976-05-28 | 1978-10-20 | Steam condensing apparatus |
Family Applications After (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA313,873A Expired CA1063362A (en) | 1976-05-28 | 1978-10-20 | Steam condensing apparatus |
Country Status (2)
Country | Link |
---|---|
US (1) | US4296802A (en) |
CA (2) | CA1059326A (en) |
Families Citing this family (24)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4506508A (en) * | 1983-03-25 | 1985-03-26 | Chicago Bridge & Iron Company | Apparatus and method for condensing steam |
US4638855A (en) * | 1983-03-31 | 1987-01-27 | Kamyr, Inc. | Heat exchange treatment of fluids |
US5067559A (en) * | 1990-09-18 | 1991-11-26 | Cdp Product Development Corporation | Diffuser screen for sparger nozzle |
US20060242970A1 (en) * | 2005-04-27 | 2006-11-02 | Foster Wheeler Usa Corporation | Low-emission natural gas vaporization system |
WO2007143798A1 (en) * | 2006-06-16 | 2007-12-21 | Richard Hunwick | Systems and methods for conserving water, cooling tower and heat exchanger |
EP2074371A4 (en) * | 2006-06-27 | 2012-07-18 | Gea Power Cooling Systems Llc | Series-parallel condensing system |
HUP0900749A2 (en) * | 2009-12-03 | 2012-01-30 | Gea Egi Energiagazdalkodasi Zrt | Cooling system for power plant |
HU228665B1 (en) * | 2009-12-03 | 2013-05-28 | Gea Egi Energiagazdalkodasi Zrt | Hybrid cooling system |
CN101936669B (en) * | 2010-09-02 | 2012-09-05 | 洛阳隆华传热科技股份有限公司 | Hybrid composite condensation method and condenser |
CN102706178A (en) * | 2011-09-06 | 2012-10-03 | 常州新德冷机有限公司 | Superheated steam temperature and pressure reducing equipment |
CN102679759B (en) * | 2012-04-01 | 2013-09-18 | 傅利江 | Direct heat exchange type steam condensing device |
RU2557823C2 (en) * | 2013-05-13 | 2015-07-27 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Казанский государственный энергетический университет" (ФГБОУ ВПО "КГЭУ") | Method of operation of combined gas-turbine unit of gas distribution system |
CN103411443B (en) * | 2013-05-31 | 2016-03-09 | 李俊峰 | The steam turbine steam exhaust cooling system of a kind of air cooling and clammy mixed running |
RU2570961C2 (en) * | 2013-12-27 | 2015-12-20 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Казанский государственный энергетический университет" (ФГБОУ ВПО "КГЭУ") | Method of operation of thermal power plant |
RU2555600C1 (en) * | 2013-12-27 | 2015-07-10 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Казанский государственный энергетический университет" (ФГБОУ ВПО "КГЭУ") | Operating method of thermal power plant |
RU2569994C2 (en) * | 2013-12-27 | 2015-12-10 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Казанский государственный энергетический университет" (ФГБОУ ВПО "КГЭУ") | Operation of thermal electric power station |
RU2562506C2 (en) * | 2013-12-27 | 2015-09-10 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Казанский государственный энергетический университет" (ФГБОУ ВПО "КГЭУ") | Method of operation of thermal power plant |
RU2555597C1 (en) * | 2013-12-27 | 2015-07-10 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Казанский государственный энергетический университет" (ФГБОУ ВПО "КГЭУ") | Operating method of thermal power plant |
RU2552481C1 (en) * | 2013-12-27 | 2015-06-10 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Казанский государственный энергетический университет" (ФГБОУ ВПО "КГЭУ") | Operating method of thermal power plant |
RU2569470C2 (en) * | 2013-12-27 | 2015-11-27 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Казанский государственный энергетический университет" (ФГБОУ ВПО "КГЭУ") | Operation of thermal electric power station |
RU2570943C2 (en) * | 2014-03-11 | 2015-12-20 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Казанский государственный энергетический университет" (ФГБОУ ВПО "КГЭУ") | Method of operation of thermal power plant |
CN104061778B (en) * | 2014-07-03 | 2017-01-11 | 刘吉生 | Energy-saving use method for pipe bundle drier |
US10577986B2 (en) | 2016-04-22 | 2020-03-03 | American Exchanger Services, Inc. | Systems and methods for improving power plant efficiency |
US20210388765A1 (en) * | 2020-06-16 | 2021-12-16 | General Electric Company | Wet dry integrated circulation cooling system |
Family Cites Families (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2545926A (en) * | 1949-06-06 | 1951-03-20 | Hudson Engineering Corp | Air and liquid cooling apparatus and method |
US2858677A (en) * | 1955-04-11 | 1958-11-04 | Marley Co | Water cooling apparatus |
DE1806656B2 (en) * | 1968-11-02 | 1971-05-13 | PROCEDURE FOR DISCHARGE OF WASTE HEAT ARISING IN INDUSTRIAL PLANTS, IN PARTICULAR IN POWER PLANTS | |
DE1925234B2 (en) * | 1969-05-17 | 1973-08-16 | GEA Luftkuhlergesellschaft Happel GmbH & Co KG, 4630 Bochum | INJECTION CONDENSATION SYSTEM WITH RECOOLING OF THE INJECTION WATER VIA AIR-COOLED COOLING ELEMENTS |
BE754270A (en) * | 1969-08-01 | 1970-12-31 | Balcke Maschbau Ag | PROCESS FOR PREVENTING THE FORMATION OF FOG ON REFRIGERATION TOWER AND REFRIGERATION TOWER FOR THE IMPLEMENTATION OF THIS PROCEDURE |
US3831667A (en) * | 1971-02-04 | 1974-08-27 | Westinghouse Electric Corp | Combination wet and dry cooling system for a steam turbine |
US3881548A (en) * | 1971-07-14 | 1975-05-06 | Westinghouse Electric Corp | Multi-temperature circulating water system for a steam turbine |
BE790513A (en) * | 1971-10-25 | 1973-02-15 | Tyeploelektroprojekt | CONDENSING DEVICE FOR STEAM TURBINE THERMAL PLANTS |
US3782451A (en) * | 1972-06-19 | 1974-01-01 | Marley Co | Hydraulic flow distribution system for multiple pass air cooled heat exchanger |
US3794304A (en) * | 1972-06-19 | 1974-02-26 | Marley Co | Pneumatic weir water level control for cooling tower hot water distribution basin |
US3878273A (en) * | 1972-10-13 | 1975-04-15 | James H Anderson | Plural water/air contact for cooling water cycle |
-
1976
- 1976-05-28 US US05/690,883 patent/US4296802A/en not_active Expired - Lifetime
- 1976-10-08 CA CA263,084A patent/CA1059326A/en not_active Expired
-
1978
- 1978-10-20 CA CA313,873A patent/CA1063362A/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
CA1063362A (en) | 1979-10-02 |
US4296802A (en) | 1981-10-27 |
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